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WO1998037168A3 - Catalyst and process for the hydrogenation of hydrocarbons - Google Patents

Catalyst and process for the hydrogenation of hydrocarbons Download PDF

Info

Publication number
WO1998037168A3
WO1998037168A3 PCT/GB1998/000409 GB9800409W WO9837168A3 WO 1998037168 A3 WO1998037168 A3 WO 1998037168A3 GB 9800409 W GB9800409 W GB 9800409W WO 9837168 A3 WO9837168 A3 WO 9837168A3
Authority
WO
WIPO (PCT)
Prior art keywords
feedstock
hydrogenation component
reaction zone
long chain
chain hydrocarbons
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/GB1998/000409
Other languages
French (fr)
Other versions
WO1998037168A2 (en
Inventor
Rafael Luis Espinoza
Andre Peter Steynberg
Samantha Harding
Johan Labuschagne
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sasol Chemicals Europe Ltd
Sasol Technology Pty Ltd
Original Assignee
Sasol Chemicals Europe Ltd
Sasol Technology Pty Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sasol Chemicals Europe Ltd, Sasol Technology Pty Ltd filed Critical Sasol Chemicals Europe Ltd
Priority to DE19882126T priority Critical patent/DE19882126T1/en
Priority to AU60000/98A priority patent/AU6000098A/en
Publication of WO1998037168A2 publication Critical patent/WO1998037168A2/en
Publication of WO1998037168A3 publication Critical patent/WO1998037168A3/en
Priority to US09/372,638 priority patent/US6278034B1/en
Priority to NO19994000A priority patent/NO994000L/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/14—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with moving solid particles
    • C10G45/16—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with moving solid particles suspended in the oil, e.g. slurries
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74—Iron group metals
    • B01J23/755—Nickel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • B01J8/224—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement
    • B01J8/226—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement internally, i.e. the particles rotate within the vessel
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/02—Boron or aluminium; Oxides or hydroxides thereof
    • C07C2521/04—Alumina
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • C07C2521/08—Silica
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74—Iron group metals
    • C07C2523/755—Nickel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S208/00—Mineral oils: processes and products
    • Y10S208/95—Processing of "fischer-tropsch" crude

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Materials Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

A process for hydrogenating long chain hydrocarbons comprises continuously feeding a feedstock (24) comprising long chain hydrocarbons into a slurry bed (12) comprising a slurry of catalyst particles in a slurrying liquid. The slurry bed is contained in a reaction zone (30) at a low level (24). A hydrogenation component is fed continuously (22) into the slurry bed, at a low level. The hydrogenation component is allowed to react with the feedstock, to hydrogenate the feedstock, as the feedstock and hydrogenation component pass upwardly through the bed (30). Hydrogenated long chain hydrocarbons are withdrawn from the reaction zone at a high level, (26) as a hydrogenated product. Any excess hydrogenation component is withdrawn from the reaction zone at a high level (48). The catalyst particles may have a size distribution between 1 and 250 microns. The catalyst may consist of a nickel component impregnated in a subatmospheric environment or a particulate alumina or silica carrier.
PCT/GB1998/000409 1997-02-20 1998-02-10 Catalyst and process for the hydrogenation of hydrocarbons Ceased WO1998037168A2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
DE19882126T DE19882126T1 (en) 1997-02-20 1998-02-10 Hydrogenation of hydrocarbons
AU60000/98A AU6000098A (en) 1997-02-20 1998-02-10 Hydrogenation of hydrocarbons
US09/372,638 US6278034B1 (en) 1997-02-20 1999-08-11 Hydrogenation of hydrocarbons
NO19994000A NO994000L (en) 1997-02-20 1999-08-19 Process of hydrogenation of hydrocarbons

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
ZA971463 1997-02-20
ZA97/1463 1997-02-20
ZA98/0586 1998-01-23
ZA9800586A ZA98586B (en) 1997-02-20 1998-01-23 "Hydrogenation of hydrocarbons".

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US09/372,638 Continuation US6278034B1 (en) 1997-02-20 1999-08-11 Hydrogenation of hydrocarbons

Publications (2)

Publication Number Publication Date
WO1998037168A2 WO1998037168A2 (en) 1998-08-27
WO1998037168A3 true WO1998037168A3 (en) 1998-11-05

Family

ID=27143727

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1998/000409 Ceased WO1998037168A2 (en) 1997-02-20 1998-02-10 Catalyst and process for the hydrogenation of hydrocarbons

Country Status (7)

Country Link
US (1) US6278034B1 (en)
AU (1) AU6000098A (en)
DE (1) DE19882126T1 (en)
MY (1) MY118373A (en)
NO (1) NO994000L (en)
WO (1) WO1998037168A2 (en)
ZA (1) ZA98586B (en)

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US6080301A (en) 1998-09-04 2000-06-27 Exxonmobil Research And Engineering Company Premium synthetic lubricant base stock having at least 95% non-cyclic isoparaffins
EP1119411B1 (en) 1998-10-05 2003-06-25 Sasol Technology (Proprietary) Limited Impregnation process for catalysts
US20030129110A1 (en) * 2001-12-04 2003-07-10 Sasol Technology (Proprietary) Limited Slurry phase apparatus
GB0214383D0 (en) * 2002-06-21 2002-07-31 Isis Innovation Catalyst
US7081555B2 (en) 2002-08-07 2006-07-25 Shell Oil Company Process for hydrogenation of aromatics in hydrocarbon feedstocks containing thiopheneic compounds
JP4552378B2 (en) * 2003-01-16 2010-09-29 住友化学株式会社 Olefin hydrogenation method
US7488601B2 (en) 2003-06-20 2009-02-10 Roche Diagnostic Operations, Inc. System and method for determining an abused sensor during analyte measurement
MY140160A (en) 2004-01-28 2009-11-30 Shell Int Research Heat exchanger for carrying out an exothermic reaction
AU2005218950B2 (en) * 2004-03-08 2008-09-04 Shell Internationale Research Maatschappij B.V. Gas distributor for a reactor
GB2412612B (en) * 2004-04-02 2008-10-29 Statoil Asa Slurry bubble column reactor
US7678732B2 (en) 2004-09-10 2010-03-16 Chevron Usa Inc. Highly active slurry catalyst composition
US7972499B2 (en) 2004-09-10 2011-07-05 Chevron U.S.A. Inc. Process for recycling an active slurry catalyst composition in heavy oil upgrading
WO2006070007A1 (en) * 2004-12-31 2006-07-06 Shell Internationale Research Maatschappij B.V. Hydrogenation catalyst and use thereof for hydrogenating fischer-tropsch endproducts
US7708877B2 (en) * 2005-12-16 2010-05-04 Chevron Usa Inc. Integrated heavy oil upgrading process and in-line hydrofinishing process
US8048292B2 (en) * 2005-12-16 2011-11-01 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US7431831B2 (en) * 2005-12-16 2008-10-07 Chevron U.S.A. Inc. Integrated in-line pretreatment and heavy oil upgrading process
US7390398B2 (en) * 2005-12-16 2008-06-24 Chevron U.S.A. Inc. Process for upgrading heavy oil using a highly active slurry catalyst composition
US7431823B2 (en) * 2005-12-16 2008-10-07 Chevron U.S.A. Inc. Process for upgrading heavy oil using a highly active slurry catalyst composition
US20070140927A1 (en) * 2005-12-16 2007-06-21 Chevron U.S.A. Inc. Reactor for use in upgrading heavy oil admixed with a highly active catalyst composition in a slurry
US7943036B2 (en) 2009-07-21 2011-05-17 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US7938954B2 (en) * 2005-12-16 2011-05-10 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US7931796B2 (en) 2008-09-18 2011-04-26 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US7431822B2 (en) * 2005-12-16 2008-10-07 Chevron U.S.A. Inc. Process for upgrading heavy oil using a reactor with a novel reactor separation system
US8372266B2 (en) * 2005-12-16 2013-02-12 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US8236170B2 (en) * 2005-12-16 2012-08-07 Chevron U.S.A. Inc. Reactor for use in upgrading heavy oil
US8435400B2 (en) * 2005-12-16 2013-05-07 Chevron U.S.A. Systems and methods for producing a crude product
AU2006336094B2 (en) * 2006-01-23 2009-12-10 Shell Internationale Research Maatschappij B.V. Hydrogenation catalyst and use thereof for hydrogenating Fischer-Tropsch endproducts
US7820120B2 (en) * 2007-12-19 2010-10-26 Chevron U. S. A. Inc. Device for a reactor and method for distributing a multi-phase mixture in a reactor
WO2009085999A2 (en) * 2007-12-19 2009-07-09 Chevron U.S.A. Inc. Reactor for heavy oil upgrade and method of use
US7927404B2 (en) * 2007-12-19 2011-04-19 Chevron U.S.A. Inc. Reactor having a downcomer producing improved gas-liquid separation and method of use
US7842262B2 (en) * 2007-12-19 2010-11-30 Chevron U.S.A. Inc. Process and apparatus for separating gas from a multi-phase mixture being recycled in a reactor
US7964153B2 (en) * 2007-12-19 2011-06-21 Chevron U.S.A. Inc. Reactor having a downcomer producing improved gas-liquid separation and method of use
US7897035B2 (en) 2008-09-18 2011-03-01 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US7897036B2 (en) * 2008-09-18 2011-03-01 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US20110017637A1 (en) * 2009-07-21 2011-01-27 Bruce Reynolds Systems and Methods for Producing a Crude Product
US7931797B2 (en) * 2009-07-21 2011-04-26 Chevron U.S.A. Inc. Systems and methods for producing a crude product
US8236169B2 (en) * 2009-07-21 2012-08-07 Chevron U.S.A. Inc Systems and methods for producing a crude product
US7935243B2 (en) 2008-09-18 2011-05-03 Chevron U.S.A. Inc. Systems and methods for producing a crude product
GB2465554B (en) * 2008-11-18 2013-03-13 Gtl F1 Ag Slurry bubble column reactor
GB2466315B (en) 2008-12-22 2013-01-09 Gtl F1 Ag Apparatus and method for conducting a Fischer-Tropsch synthesis reaction
GB2471338B (en) 2009-06-26 2014-12-24 Gtl F1 Ag Apparatus and process for three-phase reacton
US9068132B2 (en) 2009-07-21 2015-06-30 Chevron U.S.A. Inc. Hydroprocessing catalysts and methods for making thereof
US8927448B2 (en) 2009-07-21 2015-01-06 Chevron U.S.A. Inc. Hydroprocessing catalysts and methods for making thereof
US8759242B2 (en) 2009-07-21 2014-06-24 Chevron U.S.A. Inc. Hydroprocessing catalysts and methods for making thereof
US9018124B2 (en) 2010-12-30 2015-04-28 Chevron U.S.A. Inc. Hydroprocessing catalysts and methods for making thereof
CN103998573B (en) 2011-11-21 2016-08-24 沙特阿拉伯石油公司 Use slurry bed hydrotreating and the system of the raw material containing dissolved hydrogen
US9321037B2 (en) 2012-12-14 2016-04-26 Chevron U.S.A., Inc. Hydroprocessing co-catalyst compositions and methods of introduction thereof into hydroprocessing units
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CN105983377B (en) * 2015-01-30 2020-07-28 上海睿碳能源科技有限公司 Airlift Inner Loop Slurry Bed Reactor
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Also Published As

Publication number Publication date
AU6000098A (en) 1998-09-09
DE19882126T1 (en) 2000-02-24
NO994000L (en) 1999-10-13
NO994000D0 (en) 1999-08-19
ZA98586B (en) 1999-07-23
US6278034B1 (en) 2001-08-21
MY118373A (en) 2004-10-30
WO1998037168A2 (en) 1998-08-27

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